FORMED ARTICLES FROM POLYESTER RESINS

Abstract: Articles from a polyester resin obtained by melt-shaping of the resin added with a polyfunctional compound, capable of increasing the molecular weight of the resin by addition reaction in the solid state with the end groups of the resin and by upgrading treatment of the article, so as to increase by at least 0.1 dl/g the intrinsic viscosity of the starting resin.

Description: FORMED ARTICLES FROM POLYESTER RESINS The present invention relates to a new process for the pre¬ paration of articles formed of polyester resins endowed of valuable mechanical and impact strength properties. The polyester resins because of their favourable mechanical properties find wide application in the preparation of fi¬ bres and films. The resins utilized for this application ha¬ ve values of intrinsic viscosity generally between 0.6 and 0.8 dl/g. The resins are also used in blow-molding or extrusion- molding processes for the production of bottles and similar thin walled containers. The resins used in blow molding processes have a sufficien¬ tly high intrinsic viscosity to allow the realization of the injection operation. The viscosity suitable for these applications is generally between 0.7-0.8 dl/g and is obtained by solid state upgra¬ ding treatments. For the molding of articles with thick walls or with large dimension it is necessary to use resins with a not very high molecular weight to maintain the viscosity in the melt at values suitable for the molding process. The mechanical properties of the articles thus obtained are not satisfactory, because of the low molecular weight of the resin. It has been tried to obviate this difficulty by carryingoutthe molding process in the presence of small quantities of poly¬ functional compounds blended in the molten resin, capable of reacting with the resin end groups to increase the molecular weight of the same. The use of polyfunctional compounds allows to obtain molded articles in which the polymer has sufficiently high values of intrinsic viscosity to ensure good mechanical properties and impact strength. Carrying out these processes is a difficult operation becau¬ se of the necessity of using a melt with a relatively high viscosity. It is moreover difficult to control the process and to ob¬ tain formed articles with reproducible properties because of the complex reactions which occur in the melt. It is therefore desirable to have at disposal molding pro¬ cesses of easy realization which allow to obtain formed ar¬ ticleshaving high mechanical properties. It has been now unexpectedly found a melt-shaping process of polyester resins, which allows to obtain formed articles endowed of valuable mechanical properties by using in the shaping phase a melt having a not too high viscosity so as to prevent an easy resin processability. The invention process comprises a first phase in which the melt polyester resin mixed with an upgrading polyfunctional compound capable to increase the molecular weight of the re¬ sin by addition reactions in the solid state with the resin end groups is melt-shaped under temperature and duration conditions and at concentrations of the upgrading compound such as to avoid increasing the intrinsic viscosity to va¬ lues greater than about 1.0 dl/g and a second phase in which the formed article is subjected to upgrading reaction in the solid state so as to increase the intrinsic viscosity of at least 0.1 dl/g with respect to the polymer viscosity before the upgrading treatment. The resin used in the melt-shaping step has an intrinsic vi¬ scosity higher than 0.4 dl/g but generally lower than 1.0 dl/g. The polymer intrinsic viscosity in the manufactured article has values higher than about 0.7 dl/g and generally included between 0.7 and 1.8 dl/g. It has been unexpectedly found that the polymer in the for¬ med articles, having the above values of intrinsic viscosi¬ ty, shows particularly high mechanical properties such as the tensile strength and resiliency, higher than those of the polymer upgraded with processes different from that of the invention. Particularly high mechanical properties especially high not¬ ched impact strength are shown by the glass reinforced articles. The invention process is particularly suitable for the pre¬ paration of formed articles such as films, panels, plates sheets and generally thick-walled articles. For upgrading reaction in the solid state it is meant a thermal treatment carried out on the formed article, at tem¬ peratures higher than about 130°C and lower than the melting point of the resin. The treatment duration, the temperature and the concentra¬ tion of the upgrading additive are selected so as to obtain an increase of intrinsic viscosity of at least 0,1 dl/g in comparison with the intrinsic viscosity of the starting po¬ lymer used in the melt-shaping step. The upgrading reaction is carried out in inert gas stream, such as nitrogen, carbon dioxide or, if necessary,under vacuum. Regarding the films, the mechanical properties are conside¬ rably improved if the upgrading treatment is carried under stretch. The utilizable stretching ratios are generally in¬ cluded between 1:2 and 1:8. The polyester resins used in the invention process include products of polycondensation of aromatic bicarboxylic acids such as terephthalic acid or its esters such as di ethylte- rep h thalate, naphthalenbicarboxylic acids, 5-ter butyl-1,3- benzendicarboxylic acids with glycolε with 2-10 carbon atoms such asethylene glycol, 1.4-cyclohexanediol, -4 butanediol, hydroguinone. Polycondenεation products are also comprised containing, be¬ sides the units deriving from terephthalic acid or its esters, also up to 25% of all acid units, units deriving from bicarboxylic acids such as isophtalic and orthophtalic acid.Polyethyleneterephthalate and polybutyleneterephthalate are the preferred resins. The polyester resin can be added with other compatible poly¬ mers such as polycarbonates, elastomeric polyesters and po- lycaprolactone in amounts up to 20% by weight. .Recycled po¬ lyester can be used. It has been found, and it is another aspect of the inven¬ tion, that the addition of up to 5% by weight of compounds or polymers having properties of liquid crystals and contai¬ ning groups reactive with the upgrading compounds such as the OK and NI- groups improves the mechanical properties (e- lastic modulus) of the formed articles (films) subjected to upgrading under stretch. An example of polymer liquid cry¬ stals is the product sold by Hoechst Ceianese under the tra¬ de mark T CP Vectra A 950. The upgrading additives usable in the invention process lead - to the increase of the resin molecular weight by addition reactions in the solid state, with the end groups of the po¬ lyester resin. The additives are used in amount from about 0.05 to 2% by weight on the resin. The dianhydrides of the tetracarboxylic aromatic acids are the preferred additives. The dianhydride of pyromellitic acid is the preferred compound. Other representative dianhydrides are those of 3.3', 4.4'- benzophenone - tetracarboxy and, . 2,2 - bis (3,4 dicarboxylphenyl) propane acid, 3.3'-4.4'- biphenyltetracarboxy acid, bis (3.4 dicarboxyphenyl) propa- ne acid 3.3'- 4.4'- biphenyltetracarboxy acid, bis (3,4 di¬ carboxyphenyl) ether, bis (3,4 dicarboxyphenyl) sulfone and their mixtures. Dianydrides of aliphatic tetracarboxylic acids are also sui¬ table. Examples of these dianydrides are the dianydride of 1,2,3,4 cyclobutanetetracarboxylic acid and 2,3,4,5 tetra- carboxyhydrofuran acid. The blending of the resin with the additive is preferably carried out in a mono or twin screw extruder at a temperatu¬ re between 200° and 350°C. A counter rotating not intermishing twin screw extruder is preferred. The extruded polymer is subsequently pelletized and subjec¬ ted to the shaping process. The resin is melt-shaped according to the techniques inclu¬ ding extrusion blow molding, blow molding, injection- extrusion, extrusion to form sheets, tubes. Conventional additives can be blended in the polyester. Such additives include stabilizers, antioxidants, plasticizers pigments, nucleant agents, antiflame compounds, inert or reinforcing fillers such as glass fibers. In general, the addition of the glass fibers improves the notched impact strength, initial flexural modulus and brea¬ king stress of the articles obtained with the invention pro¬ cess. The use of as a little as 5% by weight of glass fibers is sufficient to increase the properties. Concentrations as high as 60% or higher can be used.Preferred concentrations are from 10 and 40% by weight. The glass fibers are preferably 0.2 to 1 mm in length. They are added to the composition in any suitable manner. For example they may be incorporated into the polyester re¬ sin before the upgrading compound is added or the molten re¬ sin, the glass fibers and the upgrading compound are mixed in an extruder. Preferably the glass fibres are added to the polyester resin premixed with melt with the upgrading com- pound. The residence time of the resin in the shaping appa¬ ratus is lower than 2 minutes, preferably comprised between 20 and 100 seconds and the barrel temperature is lower than about 300°C and higher than the melting point of the resin. PET is the preferred resin for preparing glass fibers rein¬ forced articles. The glass reinforced resins are particu¬ larly suitable for preparing food containers for dual ovena- ble applications or for any other application involving heat treatment. The following examples are given to illustrate but not to limit the invention. EXAMPLE 1 Polybutylenterephtalate having an intrinsic viscosity of 0. 587 dl/g added respectively with 0 , 3% and 0 , 5% by weight of pyromellitic dianhydride (PMDA) (respectively polymer A and polymer B) is extruded in a counter rotating twin screw extruder Haake Rheocord 90 Fison to obtain chips with a di- mater o f about 3 mm and a length of 5 mm. The polymer not added of PMDA (Polymer C) is extruded in the same way. The intrinsic viscosity after extrusion was: Polymer A IV = 0.599 dl/g Polymer B IV = 0.616 dl/g Polymer C IV = 0.580 dl/g The chips were then extruded in a mono screw extruder with filming head to mold a film with thickness of about 0.37 mm that is then subjected to an upgrading thermal treatment at 180°C for 64 h, under vacuum. The polymer intrinsic viscosity in the three different films after upgrading was: Film A IV = 1.807 dl/g Film B IV - 1.605 dl/g Film C IV = 0.821 dl/g Mechanical tests carried out on film samples have given fol¬ lowing results: FILM A B C Stress at peak MPa 58 66 30 Stress at break MPa 50 62 22 Strain at break % 6.1 11. .2 5.2 Elastic modulus MPa 950 975 967 Energy at break J 0.0128 0.0357 0.005 EXAMPLE 2 Films extruded according to example 1 were subjected to upgrading treatment at 170°C for 4h under vacuum. l * he polymer intrinsic viscosity in the films was: (in paren¬ thesis is reported the I.V. of the films before upgrading. Film A I.V. = 0.74 dl/g (0.60 dl/g) Film B I.V. = 0.77 dl/g (0.63 dl/g) Film C I.V. = 0.74 dl/g (0.57 dl/g) Mechanical tests carried out on film samples have given fol¬ lowing results: FILM B Stress at peak MPa 58 59 57 Stress at break MPa 50 62 22 Strain at break % 6.1 11.2 5.2 Elastic modulus MPa 950 975 967 Energy at break J 0.0128 0.0357 0.005 EXAMPLE 3 Films from polyethylenterephthalate (PET) chips having I.V. = 0.642 dl/g and added with 0,5% of PMDA were obtained ope¬ rating in conformity with example 1. One film was heated and stretched with a speed of 10 mm/min from 25 to 230°C under nitrogen and 1 bar of pressure and maintained under constant load of 30N between 180 and 230°C for 30 min. The stress at break, the strain at break and the elastic mo¬ dulus of film were respectively 147.5 MPa 8.6% and 4700 MPa. These values were of 67.5 MPa, 8.9% and 946 MPa for the film not subjected to upgrading/stretching and treatment. The I.V. of the polymer with film before and after upgrading respectively was of 0.64 and 0.80 dl/g The determination of the mechanical properties were carried out according to ASTM D-638. The intrinsic viscosity was determined in a solution at 60/40 by weight of phenol and tetraclorethane, operating at 25°C. EXAMPLE 4 10 Kg/h of a mixture of 99.5% by weight of crystalline PET having I.V.=0.642 dl/g and 0.5% by weight of liquid crystals TLCP Vectra A 950 (Hoechst Celanese) previously vacuum dried at 140°C for lOh and then added with 0.3% by weight of PMDA was fed into a counter rotating not intermeshing twin screw extruder and then pelletized. The extrusion conditions are as follows: Screw ratio (L/D) : 36 Screw rotation speed: 145 rpm Barrel temperature: 260°C Die type: round with 3mm diameter 5Kg/h of the so obtained chips were fed into a mono screw extruder provided with a flat die suitable for cast film production. The extrusion conditions were as follows: Screw ratio L/D = 28 Screw rotation speed = 80 rpm Barrel temperature = 265 °C Head temperature = 275°C Samples of 40 mm length were cut from the so obtained film and tested with anINSTRON tensile Tester (Mod. 4505) having a heating chamber. Operating under nitrogen at 190°C for 30 min, the samples were stretched with a rate of 1 mm/min so as to obtain a len¬ gthening of twice the original length. The obtained samples (not less than 5) were then subjected to the measuring of the tensile properties (elastic modulus, stress at break and at peak) . The determinations were carried out according to ASTM D-882 using anINSTRON tensile Tester (Mod. 4505) . The obtained results are shown in table 1, where are indica¬ ted also the film data obtained under the conditions of this example 4 from chips prepared from mixtures of: 99,5% by weight of crystalline PET (IV=0.61 dl/g) and 0.5% by weight of TLCP Vectra A 950 (Hoechst Celanese) (comparative example 1) 99,7% by weight of crystalline PET (IV=0.61 dl/g) and 0.3% by weight of PMDA (comparative test 1 of Example 4) and from crystalline PET (IV=0.61 dl/g) ; (comparati¬ ve example 2) Table 1 PRODUCT MECHANICAL PROPERTIES Modulus (MPa) Tensile strength Strain at break (MPa) % Ex. 4 4520 58 9 Cmp. 1 2562 94 13 Tex.l-Ex.4 2624 93 47 Cmp. 2 1637 62 50 LCP Vectra A 950 38000 138-241 1-3 The elastic modulus values expected for films obtained from mixtures according to example 4 and comparative 1, in the hypothesis of perfect adhesion between LCP and the polyester matrix, are respectively of 2770 and 1790 MPa. EXAMPLE 5 30 Kg/h of polyethylene terephthalate (PET) with a melting point of 253°C and intrinsic viscosity of 0,66 dl/g are con¬ tinuously fed from the polycondensation section in the melt state of PET to counterrotating and not intermeshing twin screw extruder of mm 30 in diameter, equipped with a device for outgassing. 590 g/h of a blend 20% in weight of pyromellitic dyanidride (PMDA) in crystallized powdered PET (IV-0.64 dl/g) are con¬ tinuously fed to an extruder using a gravimetric feeder. The test conditions are the following: - Pyromellitic dyanidride in melt = 0,4% weighting - Screw speed = 415 RPM - Length/Diameter ratio of the screw = 24 - Average residence time = 18-25 sec. 11 - Cylinder temperature = 283 °C - Melt temperature = 290°C A mold with a doble hole is used for the extrusion (diameter = 7 mm) A stran d pelletizer is used to obtain granules with a cylin¬ der shape having 3 mm as diameter and 5 mm as length. The intrinsic viscosity of the granules is 0.64-0.65 dl/g. 10 Kg/h of these granules are fed, after drying in a counterrota¬ ting twin screw extruder, 70 mm in diameter. L/D ratio equal to 32. After the melting of the polymer (12 L/D) the requested amount of glass fibres was fed by a lateral feeder. The re¬ maining 20 L/D length of the extruder was used to mix PET and glass fibres. Residence time in the extruder was 60-90 seconds at 270°C. The product was extruded through a 750 mm wide flat die and then gathered on 3 cooled rolls. An additional natural cooling bench was used to stabilize the formed sheets. Then a part of the sheets was subjected to upgrading at 190°C in vacuum for 12h. Mechanical characterization has been carried out on sheets after the extrusion and after the upgrading treatment. The data of the upgraded sheets are reported in the follo¬ wing table: Table 2 Composition I.V. Tensile 120 D impact dl/g modulus (GPa) strength (J/m) PET 3 . 4 PET+0.4 PMPA 3 . 5 PET+20% fibres glass 0 . 850 4 . 9-8 . 7 <* > 80 PET+30% fibres glass 0. 920 6-11 ( * ) 90 PEt+40% fibres glass 0 . 95 6 . 4 -13 . 8 (* ) 117 ( ) The higher value is referred to the direction of extru¬ sion: the lower value to an orthagonal direction. Tensile tests have been carried out using an Instron machine Series 4500 operating at 10 mm/min under room conditions on specimens cut out from original sheets. At least 5 specimens for each sample have been tested. A dynamic extensometer (12.5 mm) has been used to avoid sam¬ ples slipping between the clamps. Impact properties have been checked using an Isod impact te¬ ster Ceast using a 2 J hammer and notched specimens cut out from original sheets. At least 5 specimens for each sample were be tested. EXAMPLE 6 Results similar to those reported in Example 5 were obtained for the glass fibres reinforced sheets obtained from PET scraps having I.V.= 0.62 dl/g and melting point of 253°C.

Claims: 13 CLAIMS 1. Articles from polyester resins obtained by melt-shaping a resin having an intrinsic viscosity higher than 0.5 dl/g and lower than about 1,0 dl/g, mixed with a poly¬ functional upgrading additive capable of increasing the intrinsic viscosity of the resin by addition reaction in the solid state with the resin end groups and the¬ reafter by an upgrading treatment of the solid article at temperatures higher than 130°C but lower than the resin melting point so as to raise the resin intrinsic viscosity of at least 0.1 dl/g in respect of the Halue of the in trinsic viscosity of the polymer before the upgrading treatment. 2- Articles according to claim 1 obtained from polybuty- lenterephthalate. 3. Articles according to claim 1 and 2 where the intrinsic viscosity of the polymer in the formed article after upgrading " treatment is higher than 0.8 dl/g and prefe¬ rably than 1.0 dl/g. 4. Glass fibers reinforced articles according to claims 1,2 or 3 containing from 10 to 50% by weight of glass fibers. 5. Films in polybutylenterephthalate according to claims 1,2 or 3. 6. Films according to claims 1, 3 or 5 obtained by upgra¬ ding under stretching. 14 7. Film according to claim 6, where the resin is added with up to about 5% by weight of a compound or polymer with properties of liquid crystal. 8. Film according to claim 6, where the upgrading additive is pyromellitic anhydride.

Inventors: AL GHATTA HUSSAIN ALI KASHIF, COBROR SANDRO, SEVERINI TONINO, AL GHATTA, HUSSAIN, ALI, KASHIF, COBROR, SANDRO, SEVERINI, TONINO
Applicants: AL GHATTA HUSSAIN ALI KASHIF, COBROR SANDRO, M & G RICERCHE SPA, SEVERINI TONINO, AL GHATTA, HUSSAIN, ALI, KASHIF, COBROR, SANDRO, M. & G. RICERCHE S.P.A., SEVERINI, TONINO
Application year: 1994
Main classification: C08L67
IPC codes: B29C47, B29C55, B29C71, B29K67, C08G63, C08J3, C08J5, C08J7, C08K5, C08K7, C08L67